EP2533907B1 - System for coating, in particular painting, objects, in particular vehicle bodies - Google Patents
System for coating, in particular painting, objects, in particular vehicle bodies Download PDFInfo
- Publication number
- EP2533907B1 EP2533907B1 EP11703385.2A EP11703385A EP2533907B1 EP 2533907 B1 EP2533907 B1 EP 2533907B1 EP 11703385 A EP11703385 A EP 11703385A EP 2533907 B1 EP2533907 B1 EP 2533907B1
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- EP
- European Patent Office
- Prior art keywords
- separating
- electrode
- lower edges
- air
- plates
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05B—SPRAYING APPARATUS; ATOMISING APPARATUS; NOZZLES
- B05B14/00—Arrangements for collecting, re-using or eliminating excess spraying material
- B05B14/40—Arrangements for collecting, re-using or eliminating excess spraying material for use in spray booths
- B05B14/42—Arrangements for collecting, re-using or eliminating excess spraying material for use in spray booths using electrostatic means
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C3/00—Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
- B03C3/02—Plant or installations having external electricity supply
- B03C3/04—Plant or installations having external electricity supply dry type
- B03C3/08—Plant or installations having external electricity supply dry type characterised by presence of stationary flat electrodes arranged with their flat surfaces parallel to the gas stream
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C3/00—Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
- B03C3/02—Plant or installations having external electricity supply
- B03C3/16—Plant or installations having external electricity supply wet type
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C3/00—Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
- B03C3/34—Constructional details or accessories or operation thereof
- B03C3/40—Electrode constructions
- B03C3/45—Collecting-electrodes
- B03C3/53—Liquid, or liquid-film, electrodes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05B—SPRAYING APPARATUS; ATOMISING APPARATUS; NOZZLES
- B05B14/00—Arrangements for collecting, re-using or eliminating excess spraying material
- B05B14/40—Arrangements for collecting, re-using or eliminating excess spraying material for use in spray booths
- B05B14/46—Arrangements for collecting, re-using or eliminating excess spraying material for use in spray booths by washing the air charged with excess material
- B05B14/468—Arrangements for collecting, re-using or eliminating excess spraying material for use in spray booths by washing the air charged with excess material with scrubbing means arranged below the booth floor
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C2201/00—Details of magnetic or electrostatic separation
- B03C2201/04—Ionising electrode being a wire
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C3/00—Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
- B03C3/34—Constructional details or accessories or operation thereof
- B03C3/40—Electrode constructions
- B03C3/45—Collecting-electrodes
- B03C3/47—Collecting-electrodes flat, e.g. plates, discs, gratings
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C3/00—Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
- B03C3/34—Constructional details or accessories or operation thereof
- B03C3/74—Cleaning the electrodes
- B03C3/78—Cleaning the electrodes by washing
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/10—Greenhouse gas [GHG] capture, material saving, heat recovery or other energy efficient measures, e.g. motor control, characterised by manufacturing processes, e.g. for rolling metal or metal working
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S55/00—Gas separation
- Y10S55/46—Spray booths
Definitions
- the invention relates to a system for coating objects according to the preamble of patent claim 1.
- a partial flow of the paint which generally contains both solid and solvent and / or binder does not reach the object.
- This partial flow is called "overspray" in the professional world.
- the overspray is detected by the air flow in the coating booth and fed to a separation, so that the air can optionally be returned to the coating booth after suitable conditioning.
- wet separation systems are used.
- wet separators known from the market water flows together with the exhaust air from the cabin to an air flow accelerating nozzle. In this nozzle there is a turbulence of the flowing cabin exhaust air with the water. During this process, the overspray particles largely pass into the water, so that the air leaves the wet scrubber substantially purified and the paint overspray particles are in the water. From this they can then be recovered or disposed of.
- wet scrubbers is relatively much energy for circulation of the required quite large amount of water and to overcome the pressure difference between cabin, nozzle and disposal space needed.
- the treatment of the rinse water is costly due to the high use of paint-binding and detackifying chemicals and the Lackschlammentsorgung. Furthermore, the air absorbs a lot of moisture due to the intensive contact with the rinse water, which in turn results in a high energy consumption for the air treatment in the recirculation mode or requires discarding of the exhaust air at high moisture or solvent content.
- a plant of the type mentioned is from the US 5 264 014 A known.
- There collecting electrodes of an electrostatic working separation device are not cleaned mechanically, but by means of water, which is passed from above over the collecting electrodes. If the overspray particles are not water soluble, however, the cleaning remains incomplete.
- Object of the present invention is to provide a system for coating objects such that the operation of the electrostatic precipitator is more problem-free, in particular the overspray particles can be more easily removed from the separation surface.
- the overspray particles are thus taken up at the separation surface by a separating liquid, with which they can be transported away.
- the amounts of separation liquid required for this purpose are relatively small, so that the above-mentioned problems that occur in wet scrubbers, do not fall into the weight.
- the Abscheideomekeit must be tailored to the overspray particles; it may also contain additives which facilitate the subsequent removal of the overspray particles from the deposition liquid.
- the construction of the separator for the separating liquid is such that a feed chute is provided, which is formed in the lowermost region of two spring plates.
- a feed chute is provided, which is formed in the lowermost region of two spring plates.
- the two slide plates are provided which actively contribute, by their reciprocal movement, to discharging the separating liquid from the feed chute.
- a Clogging of the gap between the Abscheideelektrode and the spring plates reliably prevented by possibly entrained paint particles.
- the lower edges of the spring plates are crenellated or shaped like a coarse comb.
- This type of construction also contributes to the fact that the separating liquid escapes from the feed chute to the separating plates to the correct extent and in the correct distribution.
- the geometry of the "battlements" or the spaces between the comb teeth can be selected according to the respective needs.
- a device is preferably provided, with which the lower edges of the spring plates are so far away from the system at the Abscheide inhabit the Abscheidideelektrode that the contents of the feed chute can leak. In this way, a cleaning of the feed chute from time to time is possible, which requires a complete emptying of the feed chute.
- the system according to the invention is particularly suitable for painting objects.
- the articles are preferably vehicle bodies.
- FIG. 1 Reference is made, in which a painting plant for painting vehicle bodies is shown. Overall, it bears the reference numeral 1. In the upper half of a painting booth 2 is partially shown, which is configured in a known manner and therefore need not be explained in detail below.
- the vehicle bodies to be painted are perpendicular to the plane of the FIG. 1 conveyed continuously or intermittently by means of a transport system, not shown, and thereby applied from application facilities, which are also not shown, with paint.
- Conditioned air is introduced in uniform flow from this air plenum via a filter blanket in the interior of the spray booth 2. There, it flows downwards, takes on the non-adhering to the vehicle body paint overspray and leaves the Lackierkabine 2 by a large, covered by a walk-in grate 4 lower opening. 3
- the entire paint booth 2 rests on a steel structure 5, as is known per se.
- the plant area 6 comprises a separation chamber 9, which is closed on all sides by walls 8 except for the upper opening 3 and further openings for the passage of the air.
- the separation chamber 9 are two baffles 10 and 11. Das in FIG. 1 Left baffle 11 has a larger, relatively little inclined from outside to inside portion 11a and a subsequent thereto more inclined portion 11b.
- the section 10a can be pivoted from the working position shown by a solid line in a maintenance position shown in dashed lines.
- the portion 10b can be pivoted from the vertical working position to a maintenance position.
- From laterally mounted distribution channels 62 may have a Abscheidesammlungkeit on the baffles 10 and 11 in a more or less coherent layer on the upper surface flow down.
- a baffle 65 which extends curved between the wall 8a and the bottom 8b of the transitional space 12, provides a streamlined transition of the air in the transitional space 12th
- a receiving space 13 is provided for a total of the reference numeral 14 provided electrostatic separating device.
- the receiving space 13 is connected via a lower opening 15 with the transition space 12 and via an upper opening 16 with the space below the portion 10 a of the baffle 10 and from there via a horizontally oriented air duct 17 with an air collecting channel 18 in connection.
- the latter leads to an air conditioning device, not shown, with which the cleaned air is brought back to the correct temperature and humidity, so that it can be fed again to the air plenum above the spray booth 2.
- the volume of recirculated air is selected as a function of non-removable substances.
- FIGS. 2 to 6 Referenced As the perspective view of the separator 14 in FIG. 2 can be removed, this includes a housing 19, which is substantially down, front and top is open. Within the housing 19 is located next to each other a plurality of designed as inserts separation units 21 and 22, which have different widths.
- Each separation unit 21 comprises a front end plate 23 and a rear end plate 24. Between the two end plates 23 and 24, centrally connected to these, extending a plate-shaped deposition electrode 25, which is vertically aligned in the operating state. On both sides of the deposition electrode 25, a counter-electrode device 26 is provided in each case. In FIG. 3 only one of these counter electrode means 26 is shown; the second, identically formed is disposed behind the deposition electrode 25 and in FIG. 3 obscured by this.
- the counter-electrode device 26 has a lower corona region 26a, in which in the illustrated embodiment five corona wires 27 are provided, which are parallel to each other and at a distance from the deposition electrode 25 between a front end plate 23 adjacent holding rod (in FIG. 3 hidden) and a corresponding, the rear end plate 24 adjacent support rod 70 extend and are electrically connected to these support rods 70.
- corona region 26a is a field region 26b of the counter-electrode device 26.
- this field region 26b is realized by a grid-like field electrode 29, which is mounted parallel to the precipitation electrode 25 in a metallic frame 71 at a distance therefrom.
- the field electrode 29 is electrically connected to the frame 71, which in turn is again electrically connected to the support rods 70, so that therefore the field electrode 29 and the corona wires 27 are substantially at the same potential.
- Brackets 30 are used to attach the frame 71 and thus the entire counter electrode means 26 on the front end plate 23 and the rear end plate 24. All brackets 30 are formed as insulators; two brackets 30 on the front end plate 23 additionally contain high voltage connections.
- the separation unit 21 is designed as a slot; This means that it can be pulled out of the housing 19 as a unit.
- the deposition electrode 25 engages with its upper end portion of the gap 38 in the rail 36.
- a plurality of pairs of rollers 39a, 39b stored in the FIGS. 4 to 6 are arranged perpendicular to the plane of the drawing at a distance from each other.
- the deposition electrode 25 moves in the gap 38 accordingly until it finally comes off the rail 36.
- the separation unit 21 thus removed can then be maintained if necessary.
- the insertion the separation unit 21 takes place analogously in the reverse manner.
- the narrower separation units 22 change, like the FIG. 2 can be seen, with the wider separation units 21 from, where marginal always the wider separation units 21 are provided in the housing 19.
- the smaller width of the separation units 22 is explained by the fact that they do not have any counter-electrode means on either side of the deposition electrode.
- each deposition electrode 25 is assigned a counter-electrode device 26.
- all counterelectrode devices 26 cooperate with two deposition electrodes 25, one of which is associated with a wider separation unit 21 and the other with a narrower separation unit 22.
- the said outermost counter-electrode devices 26 each additionally cooperate with the inner surface of the adjacent side wall of the housing 19, which also serves as Abscheide Chemistry and is connected in accordance with potential.
- the upper side of the housing 19 of the separating device 14 is covered by an arrangement 44 of feed devices 80 with the aid of which the separating electrodes 25 of the separating units 21, 22 can be supplied from above with separating liquid.
- the main component of the feed device 80 is a feed channel 81, which surrounds the guide rail 36 and the upper region of the deposition electrode 25 and, like these, extends from the front end plate 23 to the rear end plate 24.
- the feed channel 81 comprises two angled symmetrical profiles 82, 83 whose upper, horizontally extending legs 82a, 83e abut each other in the normal state with their edges, as shown in FIGS FIGS. 4 and 5 is shown.
- the lower legs 82a, 83b of the two profiles 82, 83 converge towards each other towards the bottom, but keep their spacing from each other.
- the feed channel 81 delimited by the profiles 82, 83 and the spring plates 84, 85 is connected to a source of a separating liquid at a suitable location, which can not be seen in the drawing.
- the two profiles are each held in their end plates 23, 24 adjacent end portions by means of two angles 86, 87, the upper, substantially horizontal legs 86a, 86b extending in the direction of the median plane of the feeder 80. Their tops are, as will be clear below, actuating surfaces.
- the angle 86, 87 are about axes 88, 89th pivotable, which extend between the front end plate 23 and the rear end plate 24 and are fixed to these end plates 23, 24.
- Another axis 90 which is also mounted in the two end plates 23, 24, is rotationally and eccentrically connected to a cam 91.
- the cam 91 can by turning the axis 90 between an in FIG. 4 in which it has substantially upwards and has no contact with the angles 86, 87 and one in FIG. 6 shown position in which they the legs 86a, 86b of the angle 86, 87 down and the profiles 82, 83 apart, are rotated.
- Actuating pins 94, 95 extend in the vertical direction through guide bores in these guide blocks 92, 93.
- the actuating pins 94, 95 lying on opposite sides of the center plane of the feed device 80 are connected to one another in their upper end regions by an actuating plate 96.
- the operating plate 96 can be pushed down by an actuating mechanism, with the actuating pins 94, 95 moved downwardly.
- the lower ends of the actuating pins 94, 95 are each connected to the horizontal legs of angle sections 97, 98, whose vertical legs each carry a slide plate 99, 100.
- the slide plates 99, 100 abut with their inwardly facing surfaces on opposite sides of the deposition electrode 25. Your bottom edge may coincide with the actuator plate 96 and the actuating pin 94, 95 between an upper position, the in FIG. 4 is shown, and a lower position in FIG. 5 shown, move.
- the slide plates 99, 100 In the upper position of the FIG. 4 are the lower edges of the slide plates 99, 100 above the lower edges of the spring plates 84, 85, while in the lower position of the FIG. 5 the slide plates 99, 100, the spring plates 84, 85 slightly apart and their lower edges, the spring plates 84, 85 project beyond the bottom.
- tension springs 101, 102 which seek to pull the entire assembly of actuator plate 96, actuating pin 94, 95, angles 97, 98 and slide plates 99, 100 upwards.
- the separation device 14 was previously ready. made. This means, on the one hand, that the required high voltage is applied to the counterelectrode devices 26. On the other hand, the feed channels 81 of the various feed devices 80 have been filled with separating liquid so far that at least the space lying between the spring strips 84, 85 is filled on opposite sides of the slide plates 99, 100 or the separating electrode 25. Care is taken to ensure that this level of the separating liquid in the gutters 81 is permanently maintained.
- a contiguous layer of the deposition liquid flows down and thus arrives at the opposite separation surfaces of the deposition electrodes 25.
- the deposition liquid flows as a uniform layer further down on the deposition electrodes 25 and then drips from their lower edges into the sump 61 of the transitional space 12.
- the separating liquid is withdrawn continuously or intermittently from the sump 61 and freed of the overspray particles by a suitable method, for example by filtration. It can then be returned to the paint shop 1 for reuse.
- the separating liquid may be more or less viscous.
- the slide plates 99, 100 are provided. These are at appropriate intervals by pressing the actuator plate 96 from the in FIG. 4 shown upper in the in figure 5 moved shown lower position. In each such stroke, a given quantum of the deposition liquid is actively forced outwardly onto the lower regions of the separation surfaces of the deposition electrode 25.
- FIG. 2 An actuating mechanism with which this can be done is in FIG. 2 shown schematically and generally provided with the reference numeral 103. It comprises a arranged on the outside of the housing 19 geared motor 104, the two rods 105, 106 two shafts 107, 108 can rotate back and forth by a certain angle.
- the shafts 107, 108 run parallel to each other in the upper region of the housing 19 perpendicular to the rails 36 and the feed chutes 81.
- the shafts 107, 108 carry a rotationally locking for each separation unit 21, 22 an actuator 109, which in not further interest here with a way Actuating plate 96 of a feeder 80 cooperates.
- the actuating device 103 it is possible with the actuating device 103 to move all slider plates 84, 85 back and forth in the separating device 14 between their two positions.
- FIGS. 7 to 10 a second embodiment of a feed device is shown, with which the Abscheide perennial a Abscheideelektrode Abscheideomeeckkeit can be supplied.
- the embodiment of the FIGS. 7 to 10 is structurally simpler than that of FIGS. 1 to 6 but does essentially the same thing.
- Components of the second embodiment that correspond to those of the first are designated by the same reference numeral plus 100.
- FIGS. 8 to 10 are essentially identically recognize the one rail forming hollow section 136 with the gap 138 in the bottom.
- the upper portion of a Abscheideelektrode 125 extends through the gap 138 upwardly into the interior of the rail 136.
- roller pairs 139a, 139b mounted on the Abscheideelektrode 125 and run on the two lower flanges of the rail 136 from.
- the feeder 180 includes a feed chute 181 which is in some way connected to a source of a deposition liquid.
- the feed chute 181 is in turn bounded by two profiled sheets 182, 183 and by two spring sheets 184, 185 secured to lower legs of the profiled sheets 182, 183.
- the spring plates 184, 185 are not screwed in this case, but glued.
- FIGS. 1 to 6 are the profile sheets 182, 183 immovable and are connected at both opposite ends in each case with an end wall of the corresponding separation unit.
- the lower edges of the spring plates 184, 185 are in the normal state at the lateral Abscheide inhabit the Abscheideelektrode 125 at.
- FIGS. 7 to 10 has two slide plates 199, 200 which abut on opposite sides of the Abscheideelektrode 125 slidably and can be moved between different positions, which in the FIGS. 8 to 10 are shown.
- each angled spacer plate 210 and 211 is arranged, which has in its lower portion rectangular, downwardly projecting projections 210a and 211a, which are bent back into itself, so that in this case an edge region with a thickness that corresponds approximately to twice the sheet thickness.
- the projections 210a, 211a may have different or even equal distances from each other.
- In alignment with the distances between adjacent projections 210a, 211a are located in the slide plates 199, 200 as well as in the FIG. 7 also shown in the Abscheideelektröde 125 window 230, which allow leveling of the located on both sides of the Abscheideelektrode 125 Abscheideorganizkeit.
- the slide plates 199, 200 are moved up and down by an actuator 203, which serves as a power source a hydraulic or pneumatic short-stroke double cylinder 215 has.
- the short-stroke double cylinder 215 is composed of two Kurzhubzylindern 215a, 215b, which are arranged in opposite directions to each other and are secured together with their housings.
- the piston rod 215ba of the lower Kurzhubzylinders 215b is attached to a part 216 which in turn is fixedly connected to the housing of the separator.
- a vertically extending guide rail 217 on which a movable carriage 218 is guided.
- the carriage 218 is connected via an angle plate 219 with the piston rod 215aa of the upper Kurzhubzylinders 215a motion fit.
- FIG. 8 shows the "normal" work situation.
- this lie the lower edges of the spring plates 184, 185 at the opposite lying Abscheide lake the Abscheideelektrode 125.
- Abscheideengkeit Within the spring plates 184, 185 is Abscheideengkeit which, as in the first embodiment, is replenished as needed, in the feed chute 181 to maintain an approximately constant level.
- the lower edges of the slide plates 199, 200 are located above the lower edges of the spring plates 184, 185 and the lower edge of the spacers 210, 211 is located in even greater height.
- the slide plates 199, 200 are pushed downwards by corresponding actuation of the upper short-stroke cylinder 215a so that the lower edges slide below the lower edges of the spring plates 184, 185, like this in FIG. 9 is shown.
- a certain amount of the separating liquid is actively brought down from the feed chute 181 to the opposite separation surfaces of the deposition electrode 125.
- the lower edges of the spacer plates 210, 211 remain at a height such that they have no influence on the position and shape of the spring plates 184, 185.
- Positions shown change the slide plates 199, 200 and - in the same cycle hereby - the spacer plates 210, 211 back and forth.
- the deposition liquid contained in the feed chute 181 can easily drain through the spaces between the protrusions 210a, 211a.
- FIG. 7 shown perspective of the feeder 180 is a distinctive feature recognizable, which also in the embodiment of FIGS. 1 to 6 could be realized:
- the lower edge of the spring plates 184, 185 is namely there is not straight but crenellated.
- the spring plates 184, 185 thus rest against the precipitation electrode 125 only with the lower edges of the crenellated, downwardly pointing projections.
- This measure also serves to promote the flow of separating liquid out of the guide channel 181, in particular when the separating liquid is relatively viscous.
Landscapes
- Electrostatic Separation (AREA)
- Details Or Accessories Of Spraying Plant Or Apparatus (AREA)
- Electrostatic Spraying Apparatus (AREA)
- Coating Apparatus (AREA)
Description
Die Erfindung betrifft eine Anlage zum Beschichten von Gegenständen nach dem Oberbegriff des Patentanpruchs 1.The invention relates to a system for coating objects according to the preamble of
Bei der manuellen oder automatischen Applikation von Lacken auf Gegenständen gelangt ein Teilstrom des Lackes, der im Allgemeinen sowohl Festkörper als auch Lösemittel und/oder Bindemittel enthält, nicht auf den Gegenstand. Dieser Teilstrom wird in der Fachwelt "Overspray" genannt. Der Overspray wird von dem Luftstrom in der Beschichtungskabine erfasst und einer Abscheidung zugeführt, so dass die Luft gegebenenfalls nach einer geeigneten Konditionierung wieder in die Beschichtungskabine zurückgeleitet werden kann.In the manual or automatic application of paints on objects, a partial flow of the paint, which generally contains both solid and solvent and / or binder does not reach the object. This partial flow is called "overspray" in the professional world. The overspray is detected by the air flow in the coating booth and fed to a separation, so that the air can optionally be returned to the coating booth after suitable conditioning.
Insbesondere bei Anlagen mit größerem Lackverbrauch, beispielsweise bei Anlagen zum Lackieren von Fahrzeugkarosserien, kommen bevorzugt Nassabscheidesysteme zum Einsatz. Bei vom Markt her bekannten Nassabscheidern fließt Wasser gemeinsam mit der von oben kommenden Kabinenabluft zu einer die Luftströmung beschleunigenden Düse. In dieser Düse findet eine Verwirbelung der durchströmenden Kabinenabluft mit dem Wasser statt. Bei diesem Vorgang treten die Overspray-Partikel weitgehend in das Wasser über, so dass die Luft den Nassabscheider im Wesentlichen gereinigt verlässt und sich die Lackoverspray-Partikel im Wasser befinden. Aus diesem können sie dann wiedergewonnen oder entsorgt werden. Bei bekannten Nassabscheidern wird verhältnismäßig viel Energie zur Umwälzung der erforderlichen recht großen Wassermenge und zur Überwindung der Druckdifferenz zwischen Kabine, Düse und Entsorgungsraum benötigt. Die Aufbereitung des Spülwassers ist durch den hohen Einsatz an lackbindenden und entklebenden Chemikalien und durch die Lackschlammentsorgung kostenintensiv. Weiterhin nimmt die Luft durch den intensiven Kontakt mit dem Spülwasser sehr viel Feuchtigkeit auf, was im Umluftbetrieb wiederum einen hohen Energieverbrauch für die Luftaufbereitung zur Folge hat bzw. bei hohem Feuchte- oder Lösungsmittelgehalt das Verwerfen der Abluft erfordert.Especially in systems with greater paint consumption, for example in systems for painting vehicle bodies, preferably wet separation systems are used. In the case of wet separators known from the market, water flows together with the exhaust air from the cabin to an air flow accelerating nozzle. In this nozzle there is a turbulence of the flowing cabin exhaust air with the water. During this process, the overspray particles largely pass into the water, so that the air leaves the wet scrubber substantially purified and the paint overspray particles are in the water. From this they can then be recovered or disposed of. In known wet scrubbers is relatively much energy for circulation of the required quite large amount of water and to overcome the pressure difference between cabin, nozzle and disposal space needed. The treatment of the rinse water is costly due to the high use of paint-binding and detackifying chemicals and the Lackschlammentsorgung. Furthermore, the air absorbs a lot of moisture due to the intensive contact with the rinse water, which in turn results in a high energy consumption for the air treatment in the recirculation mode or requires discarding of the exhaust air at high moisture or solvent content.
Bei vom Markt her bekannten Vorrichtungen wird demgegenüber auf trockenem Weg abgeschieden, indem von der vorbeiströmenden Kabinenluft mitgeführte Overspray-Partikel durch die Gegenelektrodeneinrichtung der elektrostatisch arbeitenden Abscheidevorrichtung ionisiert werden und aufgrund des zwischen der Abscheideelektrode und der Gegenelektrodeneinrichtung aufgebauten elektrischen Felds zur Abscheidefläche der Abscheideelektrode wandern, an welcher sie sich abscheiden.In the case of devices known from the market, by contrast, it is deposited on a dry route by ionizing overspray particles entrained by the passing cabin air through the counterelectrode device of the electrostatically operating separation device and moving to the separation surface of the deposition electrode due to the electric field established between the deposition electrode and the counterelectrode device which they separate.
Bei den bekannten Anlagen werden die an der Abscheidefläche haftenden Overspray-Partikel mechanisch von dieser abgestreift und abtransportiert.In the known systems, the adhering to the separation surface overspray particles are mechanically stripped and transported away from this.
Eine Anlage der eingangs genannten Art ist aus der
Aufgabe der vorliegenden Erfindung ist es, eine Anlage zur Beschichtung von Gegenständen derart auszubilden, dass der Betrieb der elektrostatischen Abscheidevorrichtung problemfreier ist, insbesondere die Overspray-Partikel leichter von der Abscheidefläche entfernt werden können.Object of the present invention is to provide a system for coating objects such that the operation of the electrostatic precipitator is more problem-free, in particular the overspray particles can be more easily removed from the separation surface.
Diese Aufgabe wird erfindungsgemäß durch eine Anlage mit den im Patentanspruch 1 angegebenen Merkmalen gelöst.This object is achieved by a system with the features specified in
Wie im Stand der Technik bekannt, werden also die Overspray-Partikel an der Abscheidefläche von einer Abscheideflüssigkeit aufgenommen, mit der sie abtransportiert werden können. Die Mengen der hierfür benötigten Abscheideflüssigkeit sind verhältnismäßig gering, so dass die oben geschilderten Probleme, die bei Nassabscheidern auftreten, nicht ins Gewicht fallen. Selbstverständlich muss die Abscheideflüssigkeit auf die Overspray-Partikel abgestimmt sein; sie kann auch Zusätze enthalten, welche die nachträgliche Entfernung der Overspray-Partikel aus der Abscheideflüssigkeit erleichtern.As is known in the prior art, the overspray particles are thus taken up at the separation surface by a separating liquid, with which they can be transported away. The amounts of separation liquid required for this purpose are relatively small, so that the above-mentioned problems that occur in wet scrubbers, do not fall into the weight. Of course, the Abscheideflüssigkeit must be tailored to the overspray particles; it may also contain additives which facilitate the subsequent removal of the overspray particles from the deposition liquid.
Erfindungsgemäß ist die Bauweise der Zuführeinrichtung für die Abscheideflüssigkeit derart, dass eine Zuführrinne vorgesehen ist, die im untersten Bereich von zwei Federblechen gebildet ist. Dies stellt eine besonders einfache Art dar, die Abscheideflächen der Abscheideelektrode mit Abscheideflüssigkeit zu versorgen. Letztere "leckt" einfach durch den nicht ganz dichten Spalt zwischen den unteren Rändern der Federbleche und den Abscheideflächen der Abscheideelektrode hindurch.According to the invention, the construction of the separator for the separating liquid is such that a feed chute is provided, which is formed in the lowermost region of two spring plates. This is a particularly simple way to provide the Abscheideflächen the Abscheideelektrode with Abscheideflüssigkeit. The latter simply "leaks" through the not quite tight gap between the lower edges of the spring plates and the separation surfaces of the deposition electrode.
Um sicherzustellen, dass auch bei höherviskosen Abscheideflüssigkeiten ein ausreichendes, kontinuierliches und flächiges Abströmen aus der Zuführrinne erfolgt, sind die beiden Schieberbleche vorgesehen, die durch ihre reziprozierende Bewegung aktiv zum Austragen der Abscheideflüssigkeit aus der Zuführrinne beitragen. Außerdem wird ein Verstopfen des Spaltes zwischen der Abscheideelektrode und den Federblechen durch ggfs. mitgeführte Lackpartikel zuverlässig verhindert.In order to ensure that sufficient, continuous and flat outflow from the feed chute takes place, even in the case of relatively high-viscosity separation liquids, the two slide plates are provided which actively contribute, by their reciprocal movement, to discharging the separating liquid from the feed chute. In addition, a Clogging of the gap between the Abscheideelektrode and the spring plates reliably prevented by possibly entrained paint particles.
Bei einer bevorzugten Ausführungsform der erfindungsgemäßen Anlage sind die unteren Ränder der Federbleche zinnenartig bzw. nach Art eines groben Kammes geformt. Auch diese Bauweise trägt dazu bei, dass die Abscheideflüssigkeit im richtigen Maße und in der richtigen Verteilung aus der Zuführrinne auf die Abscheidebleche austritt. Die Geometrie der "Zinnen" bzw. der Zwischenräume zwischen den Kammzinken kann entsprechend den jeweiligen Bedürfnissen gewählt werden.In a preferred embodiment of the system according to the invention, the lower edges of the spring plates are crenellated or shaped like a coarse comb. This type of construction also contributes to the fact that the separating liquid escapes from the feed chute to the separating plates to the correct extent and in the correct distribution. The geometry of the "battlements" or the spaces between the comb teeth can be selected according to the respective needs.
Zusätzlich ist vorzugsweise eine Einrichtung vorgesehen, mit welcher die unteren Ränder der Federbleche von der Anlage an den Abscheideflächen der Abscheideelektrode so weit weg bewegbar sind, dass der Inhalt der Zuführrinne auslaufen kann. Auf diese Weise ist eine Reinigung der Zuführrinne von Zeit zu Zeit möglich, die eine vollständige Entleerung der Zuführrinne voraussetzt.In addition, a device is preferably provided, with which the lower edges of the spring plates are so far away from the system at the Abscheideflächen the Abscheidideelektrode that the contents of the feed chute can leak. In this way, a cleaning of the feed chute from time to time is possible, which requires a complete emptying of the feed chute.
Die erfindungsgemäße Anlage eignet sich besonders zum Lackieren von Gegenständen.The system according to the invention is particularly suitable for painting objects.
Bei den Gegenständen handelt es sich vorzugsweise um Fahrzeugkarosserien.The articles are preferably vehicle bodies.
Ausführungsbeispiele der Erfindung werden nachstehend anhand der Zeichnung näher erläutert. Es zeigen;
Figur 1- einen vertikalen Teilschnitt durch eine Lackieranlage zum Lackieren von Fahrzeugkarosserien;
Figur 2- perspektivisch eine elektrostatische Abscheidevorrichtung für Lack-Overspray, die in der Lackieranlage von
verwendet wird;Figur 1 Figur 3- perspektivisch eine erste Art einer Abscheideeinheit aus der Abscheidevorrichtung der
;Figur 2 - Figuren 4 bis 6
- die Stirnansicht einer Zuführeinrichtung für eine Abscheideflüssigkeit und einer zugeordneten Abscheideelektrode in unterschiedlichen Betriebspositionen;
Figur 7- perspektivisch ein alternatives Ausführungsbeispiel einer Zuführeinrichtung für eine Abscheideflüssigkeit;
Figuren 8 bis 10- in der Stirnansicht die Zuführeinrichtung der
, erneut in unterschiedlichen Betriebspositionen zusammen mit einer Betätigungseinrichtung.Figur 7
- FIG. 1
- a vertical section through a paint shop for painting vehicle bodies;
- FIG. 2
- in perspective, an electrostatic precipitator for paint overspray in the paint shop of
FIG. 1 is used; - FIG. 3
- perspective view of a first type of separation unit from the deposition of the
FIG. 2 ; - FIGS. 4 to 6
- the front view of a supply of a separating liquid and an associated Abscheidelektrode in different operating positions;
- FIG. 7
- in perspective, an alternative embodiment of a delivery device for a Abscheideflüssigkeit;
- FIGS. 8 to 10
- in the front view, the feeder of
FIG. 7 , again in different operating positions together with an actuator.
Zunächst wird auf
Nicht eigens dargestellt ist außerdem ein Luftplenum, welches sich oberhalb der Lackierkabine 2 befindet.Not specifically shown is also a Luftplenum, which is located above the
Konditionierte Luft wird in gleichmäßigem Strom aus diesem Luftplenum über eine Filterdecke in den Inneraum der Lackierkabine 2 eingebracht. Dort fließt sie nach unten, nimmt den nicht an den Fahrzeugkarosserien haftenden Lack-Overspray auf und verlässt die Lackierkabine 2 durch eine großflächige, durch einen begehbaren Gitterrost 4 abgedeckte untere Öffnung 3.Conditioned air is introduced in uniform flow from this air plenum via a filter blanket in the interior of the
Die gesamte Lackierkabine 2 ruht auf einem Stahlbau 5, wie dies an und für sich bekannt ist.The
Unterhalb der Lackierkabine 2 befindet sich ein Anlagenbereich 6, in welchem die die Lackierkabine 2 über die Öffnung 3 verlassende Overspray-Partikel-beladene Luft wieder gereinigt wird. Der Anlagenbereich 6 umfasst einen Abscheideraum 9, der bis auf die obere Öffnung 3 und weitere der Durchführung der Luft dienende Öffnungen allseits durch Wände 8 abgeschlossen ist. Innerhalb des Abscheideraumes 9 befinden sich zwei Leitbleche 10 und 11. Das in
Aus seitlich angebrachten Verteilerrinnen 62 kann eine Abscheideflüssigkeit auf die Leitbleche 10 und 11 in einer mehr oder weniger zusammenhängenden Schicht an deren oberer Fläche nach unten fließen.From laterally mounted
Unterhalb des von den beiden Leitblechen 10 und 11 auf gegenüberliegenden Seiten begrenzten Raumes befindet sich ein Übergangsraum 12. Ein Leitblech 65, welches sich gekrümmt zwischen der Wand 8a und dem Boden 8b des Übergangsraumes 12 erstreckt, sorgt für einen strömungsgünstigen Übergang der Luft in den Übergangsraum 12.Below the bounded by the two
Oberhalb des in
Zur Beschreibung der Abscheidevorrichtung 14 wird nunmehr auf die
Der grundsätzliche Aufbau der breiteren Abscheideeinheiten 21 ist der
Die Gegenelektrodeneinrichtung 26 weist einen unteren Koronabereich 26a auf, in dem im dargestellten Ausführungsbeispiel fünf Koronadrähte 27 vorgesehen sind, die parallel zueinander und in Abstand zu der Abscheideelektrode 25 zwischen einer der vorderen Stirnplatte 23 benachbarten Haltestange (in
Oberhalb des Koronabereiches 26a befindet sich ein Feldbereich 26b der Gegenelektrodeneinrichtung 26. Körperlich ist dieser Feldbereich 26b durch eine gitterartige Feldelektrode 29 verwirklicht, die parallel zur Abscheideelektrode 25, in Abstand zu dieser, in einem metallischen Rahmen 71 montiert ist. Die Feldelektrode 29 ist mit dem Rahmen 71 elektrisch verbunden, der seinerseits wieder mit den Haltestangen 70 elektrisch verbunden ist, so dass also die Feldelektrode 29 und die Koronadrähte 27 im Wesentlichen auf demselben Potential liegen.Above the
Halterungen 30 dienen der Befestigung des Rahmens 71 und damit der gesamten Gegenelektrodeneinrichtung 26 an der vorderen Stirnplatte 23 und der hinteren Stirnplatte 24. Alle Halterungen 30 sind als Isolatoren ausgebildet; zwei Halterungen 30 an der vorderen Stirnplatte 23 enthalten zusätzlich Hochspannungsanschlüsse.
Wie bereits oben erwähnt, ist die Abscheideeinheit 21 als Einschub ausgebildet; dies heißt, dass sie als Einheit aus dem Gehäuse 19 herausgezogen werden kann.As already mentioned above, the
Gehalten wird jede Abscheideeinheit 21 innerhalb des Gehäuses von einem eine Schiene bildenden Hohlprofil 36, in dessen Unterseite ein durchgehender Spalt 38 gebildet ist. Dies ist insbesondere den
Die Abscheideelektrode 25 durchgreift mit ihrem oberen Endbereich den Spalt 38 in der Schiene 36. An dem nach oben über den Spalt 38 überstehenden Bereich der Abscheideelektrode 25 ist eine Vielzahl von Rollenpaaren 39a, 39b gelagert, die in den
Die schmäleren Abscheideeinheiten 22 wechseln, wie der
Aufgrund der alternierenden Anordnung und der beiden Arten von Abscheideeinheiten 21, 22 innerhalb der Abscheidevorrichtung 14 ist gewährleistet, dass jeweils beiden Abscheideflächen jeder Abscheideelektrode 25 eine Gegenelektrodeneinrichtung 26 zugeordnet ist. Mit Ausnahme der äußersten Gegenelektrodeneinrichtungen 26 an den randständigen breiten Abscheideeinheiten 21 arbeiten auf diese Weise alle Gegenelektrodeneinrichtungen 26 mit zwei Abscheideelektroden 25 zusammen, wovon eine einer breiteren Abscheideeinheit 21 und die andere einer schmäleren Abscheideeinheit 22 zugeordnet ist. Die genannten äußersten Gegenelektrodeneinrichtungen 26 arbeiten jeweils zusätzlich mit der Innenfläche der benachbarten Seitenwand des Gehäuses 19 zusammen, die ebenfalls als Abscheidefläche dient und potentialmäßig entsprechend geschaltet ist.Due to the alternating arrangement and the two types of
Die Oberseite des Gehäuses 19 der Abscheidevorrichtung 14 wird von einer Anordnung 44 aus Zuführeinrichtungen 80 abgedeckt mit deren Hilfe den Abscheideelektroden 25 der Abscheideeinheiten 21, 22 von oben her Abscheideflüssigkeit zugeführt werden kann.The upper side of the
Zur näheren Beschreibung einer dieser Zuführungen 80 wird nunmehr erneut auf die
Hauptbestandteil der Zuführeinrichtung 80 ist eine Zuführrinne 81, welche die Führungsschiene 36 und den oberen Bereich der Abscheideelektrode 25 umgibt und sich ebenso wie diese von der vorderen Stirnplatte 23 bis zur hinteren Stirnplatte 24 erstreckt. Die Zuführrinne 81 umfasst zwei gewinkelte symmetrische Profile 82, 83 deren obere, waagerecht verlaufende Schenkel 82a, 83e im Normalzustand mit ihren Rändern aneinanderstoßen, wie dies in den
Die von den Profilen 82, 83 und den Federblechen 84, 85 begrenzte Zuführrinne 81 ist an einer geeigneten Stelle, die in der Zeichnung nicht erkennbar ist, mit einer Quelle einer Abscheideflüssigkeit verbunden.The
Die beiden Profile sind jeweils in ihren den Stirnplatten 23, 24 benachbarten Endbereichen mit Hilfe zweier Winkel 86, 87 gehalten, deren obere, im Wesentlichen horizontale Schenkel 86a, 86b sich in Richtung auf die Mittelebene der Zuführeinrichtung 80 erstrecken. Ihre Oberseiten stellen, wie weiter unten noch deutlich wird, Betätigungsflächen dar. Die Winkel 86, 87 sind um Achsen 88, 89 verschwenkbar, die sich zwischen der vorderen Stirnplatte 23 und der hinteren Stirnplatte 24 erstrecken und an diesen Stirnplatten 23, 24 befestigt sind.The two profiles are each held in their
Eine weitere Achse 90, die ebenfalls in den beiden Stirnplatten 23, 24 gelagert ist, ist drehschlüssig und exzentrisch mit einer Kurvenscheibe 91 verbunden. Die Kurvenscheibe 91 kann durch Verdrehen der Achse 90 zwischen einer in
Auf den Außenseiten der beiden vertikalen Schenkel der Schiene 36 sind zwei Führungsblöcke 92, 93 befestigt. Durch Führungsbohrungen in diesen Führungsblöcken 92, 93 verlaufen in vertikaler Richtung Betätigungsbolzen 94, 95. Die jeweils auf gegenüberliegenden Seiten der Mittelebene der Zuführeinrichtung 80 liegenden Betätigungsbolzen 94, 95 sind in ihren oberen Endbereichen durch eine Betätigungsplatte 96 miteinander verbunden. Die Betätigungsplatte 96 kann durch einen Betätigungsmechanismus nach unten gedrückt werden, wobei die Betätigungsbolzen 94, 95 nach unten bewegt werden.On the outer sides of the two vertical legs of the
Die unteren Enden der Betätigungsbolzen 94, 95 sind jeweils mit den horizontalen Schenkeln von Winkelprofilen 97, 98 verbunden, deren vertikale Schenkel jeweils ein Schieberblech 99, 100 tragen. Die Schieberbleche 99, 100 liegen mit ihren nach innen weisenden Flächen an gegenüberliegenden Seiten der Abscheideelektrode 25 an. Ihr unterer Rand kann sich gemeinsam mit der Betätigungsplatte 96 und den Betätigungsbolzen 94, 95 zwischen einer oberen Position, die in
Zwischen den Führungsblöcken 92, 93 und den horizontalen Schenkeln der Winkelprofile 97, 98 wirken jeweils Zugfedern 101, 102, welche die gesamte Anordnung aus Betätigungsplatte 96, Betätigungsbolzen 94, 95, Winkeln 97, 98 und Schieberblechen 99, 100 nach oben zu ziehen suchen.Between the guide blocks 92, 93 and the horizontal legs of the
Die oben beschriebene Lackieranlage 1 und insbesondere der deren Luftreinigung dienende Anlagenbereich 6 arbeiten wie folgt:
- Der beim Lackieren der Fahrzeugkarosserie in
der Lackierkabine 2 entstehende Overspray wird von dem Luftstrom, der dieLackierkabine 2 von oben nach unten durchströmt, aufgenommen und mitgeführt. Der Luftstrom durchtritt den Rost 4 und gelangt auf diese Weise inden Abscheideraum 9. Er trifft dort auf dieLeitbleche 10, 11 bzw. auf die über diese gleichmäßig abströmende Abscheideflüssigkeit. Bereits an dieser Stelle wird von der Abscheideflüssigkeit ein großer Teil der Overspray-Partikel aufgenommen. Die Abscheideflüssigkeit strömt entlang der Leitbleche 11, 10 nach unten und sammelt sich in einem Sumpf 61 im unteren Bereich desÜbergangsraumes 12.
- The resulting overspray when painting the vehicle body in the
spray booth 2 is received and carried by the air flow, which flows through thespray booth 2 from top to bottom. The air stream passes through the grate 4 and in this way enters theseparation chamber 9. It meets theguide plates 10, 11 or the separating liquid flowing off uniformly there. Already at this point a large part of the overspray particles is taken up by the separating liquid. The separating liquid flows down along theguide plates 11, 10 and collects in asump 61 in the lower region of thetransitional space 12.
Auch die Luft, die nach wie vor mit Overspray-Partikeln beladen ist, wird trichterartig in den Übergangsraum 12 geführt, dort zunächst um 90° umgeleitet und sodann aus dem Übergangsraum 12 durch eine erneute 90°-Umlenkung von unten her in die untere Einlassöffnung 15 des Gehäuses 19 der Abscheidevorrichtung 14 eingeführt. Der Abscheideraum 9 und der Übergangsraum 12 bilden so einen Luftweg zwischen der Auslassöffnung 3 der Lackierkabine 2 und der Einlassöffnung 15 der Abscheidevorrichtung 14.Even the air, which still contains overspray particles is loaded, is funnel-like led into the
Die Abscheidevorrichtung 14 wurde zuvor betriebsbereit. gemacht. Dies bedeutet zum einen, dass an die Gegenelektrodeneinrichtungen 26 die erforderliche Hochspannung angelegt wird. Zum anderen wurden die Zuführrinnen 81 der verschiedenen Zuführeinrichtungen 80 so weit mit Abscheideflüssigkeit gefüllt, dass zumindest der zwischen den Federblechen 84, 85 liegende Raum auf gegenüberliegenden Seiten der Schieberbleche 99, 100 bzw. der Abscheideelektrode 25 gefüllt ist. Dabei wird Sorge dafür getragen, dass dieses Niveau der Abscheideflüssigkeit in den Rinnen 81 dauerhaft aufrecht erhalten bleibt.The
Zwischen den unteren Rändern der Federbleche 84, 85 fließt eine zusammenhängend Schicht der Abscheideflüssigkeit nach unten und gelangt auf diese Weise auf die gegenüberliegenden Abscheideflächen der Abscheideelektroden 25. Die Abscheideflüssigkeit fließt als gleichmäßige Schicht weiter auf den Abscheideelektroden 25 nach unten und tropft dann von deren unteren Rändern in den Sumpf 61 des Übergangsraumes 12 ab.Between the lower edges of the
Die Abscheideflüssigkeit wird kontinuierlich oder intermitierend aus dem Sumpf 61 abgezogen und durch ein geeignetes Verfahren, beispielsweise durch Filtration, von den Overspray-Partikeln befreit. Sie kann dann zur Wiederverwendung in die Lackieranlage 1 zurückgeleitet werden.The separating liquid is withdrawn continuously or intermittently from the
Die mit Overspray-Partikeln beladene Luft tritt, wie oben schon erwähnt, in das Gehäuse 19 der Abscheidevorrichtung 14 ein. Sie und insbesondere die von ihr mitgeführten Overspray-Partikel werden im Bereich der Koronadrähte 27 der verschiedenen Gegenelektrodeneinrichtungen 26 ionisiert und im Bereich der Feldelektroden 29 der Gegenelektrodeneinrichtungen 26 in Richtung in die auf Massepotential liegende zugeordnete Abscheideelektrode 25 gezogen. Die Overspray-Partikel werden dabei von der Abscheideflüssigkeit, die von oben über die Abscheidefläche strömt, aufgenommen.The laden with overspray particles air enters, as already mentioned above, in the
Luft und Abscheideflüssigkeit fließen auf diese Weise im Gegenstrom. Dies hat zur Folge, dass im unteren Bereich der Abscheideelektroden 25, wo die Verschmutzung der Luft mit Overspray-Partikeln am größten ist, auch die am stärksten mit abgeschiedenen Overspray-Partikeln beladene Abscheideflüssigkeit strömt. Umso weiter die Luft sich nach oben bewegt, umso reiner wird sie. Entsprechend wird auch die über die Abscheideelektroden 25 fließende Abscheideflüssigkeit sauberer, so dass die Luft, welche die Abscheidevorrichtung 14 nach oben verlässt, ein Höchstmaß an Sauberkeit erreicht hat. Sie kann dann ohne Weiteres über den Luftkanal 17 und den Sammel-Abführkanal 18 der Rekonditionierung und von dort erneut der Lackierkabine 2 zugeführt werden.Air and separation liquid flow in this way in countercurrent. This has the consequence that in the lower region of the
Die Abscheideflüssigkeit kann mehr oder weniger viskos sein. Um das Ausströmen der Abscheideflüssigkeit aus den Zuführrinnen 81 an den unteren Rändern der Federbleche 84, 85 vorbei zu fördern, sind die Schieberbleche 99, 100 vorgesehen. Diese werden in entsprechenden Zeitabständen durch Drücken auf die Betätigungsplatte 96 aus der in
Ein Betätigungsmechanismus, mit dem dies geschehen kann, ist in
Von Zeit zu Zeit kann es erforderlich werden, den Innenraum der Zuführrinnen 81 zu reinigen. Dann wird die Kurvenscheibe 91 aus der in
In den
In den
Anders als beim Ausführungsbeispiel der
Die unteren Ränder der Federbleche 184, 185 liegen im Normalzustand an den seitlichen Abscheideflächen der Abscheideelektrode 125 an.The lower edges of the
Auch das Ausführungsbeispiel der
Auf den Außenflächen der beiden Schieberbleche 199, 200 ist jeweils ein gewinkeltes Distanzblech 210 bzw. 211 angeordnet, das in seinem unteren Bereich rechteckige, nach unten ragende Vorsprünge 210a bzw. 211a aufweist, die in sich zurückgebogen sind, so dass hier im Ergebnis ein Randbereich mit einer Dicke entsteht, die etwa der doppelten Blechstärke entspricht. Die Vorsprünge 210a, 211a können unterschiedliche oder auch gleiche Abstände von einander aufweisen. Fluchtend mit den Abständen zwischen benachbarten Vorsprüngen 210a, 211a befinden sich in den Schieberblechen 199, 200 sowie in der in
Die oberen, horizontal umgebogenen Schenkel der Distanzbleche 210, 211 sind gemeinsam mit oberen, horizontal umgebogenen Schenkeln der Schieberbleche 199, 200 an Klötzen 212, 213 befestigt, zwischen denen sich die Abscheideelektrode 125 gleitend hindurchbewegen kann. In dem in den
Die Schieberbleche 199, 200 werden von einer Betätigungseinrichtung 203 auf- und abbewegt, die als Kraftquelle einen hydraulischen oder pneumatischen Kurzhub-Doppelzylinder 215 aufweist. Der Kurzhub-Doppelzylinder 215 ist aus zwei Kurzhubzylindern 215a, 215b zusammengesetzt, die gegensinnige zueinander angeordnet sind und mit ihren Gehäusen aneinander befestigt sind. Die Kolbenstange 215ba des unteren Kurzhubzylinders 215b ist an einem Teil 216 befestigt, das seinerseits fest mit dem Gehäuse der Abscheidevorrichtung verbunden ist.The
Ebenfalls starr an dem Gehäuse angebracht ist eine vertikal verlaufende Führungsschiene 217, auf welcher ein verfahrbarer Schlitten 218 geführt ist. Der Schlitten 218 ist über ein Winkelblech 219 mit der Kolbenstange 215aa des oberen Kurzhubzylinders 215a bewegungsschlüssig verbunden.Also mounted rigidly on the housing is a vertically extending
Zwischen dem Schlitten 218 und einem auf der gegenüberliegenden Seite der Abscheidevorrichtung vorgesehenen, entsprechenden Schlitten, der in der Zeichnung nicht dargestellt ist, verläuft eine Stange 220, an der mehrere nach unten ragende Mitnehmerarme 221 befestigt sind. Für jede Abscheideeinheit ist ein derartiger Mitnehmerarm 221 vorgesehen. Er greift mit einem horizontal verlaufenden Mitnehmerstift 222 in die Mitnahmeöffnung 214 des Klotzes 213 der entsprechenden Abscheideeinheit ein. Ersichtlich können durch Betätigung des Kurzhub-Doppelzylinders 215 alle Schieberbleche 199, 200 gemeinsam mit allen Distanzblechen 210, 211 auf- und abbewegt werden, wie dies nachstehend noch näher erläutert wird.Between the
Um nun das Ausfließen der Abscheideflüssigkeit aus der Zuführrinne 181 bei Bedarf zu fördern, werden die Schieberbleche 199, 200 durch entsprechende Betätigung des oberen Kurzhubzylinders 215a so weit nach unten geschoben, dass die unteren Ränder sich unter die unteren Ränder der Federbleche 184, 185 schieben, wie dies in
Wird eine Reinigung der Zuführrinne 181 gewünscht, werden mit Hilfe des unteren Kurzhubzylinders 215b die Schieberbleche 199, 200 mit den Distanzblechen 210, 211 so weit nach unten geschoben, bis die unteren, in der Dicke vergrößerten Randbereiche der Distanzbleche 210, 211 die unteren Ränder der Federbleche 184, 185 auseinanderbiegen. Nun kann die in der Zuführrinne 181 befindliche Abscheideflüssigkeit durch die Zwischenräume zwischen den Vorsprüngen 210a, 211a leicht ablaufen.If a cleaning of the
In der in
Claims (5)
- A system (1) for coating objects having:a) a coating booth (2) in which the objects may be acted upon by coating material and through which an air stream can be guided which takes up overspray particles of the coating material and conveys them away;b) an electrostatically operating separating device (14) whereof a housing (19) has an inlet opening (15) for the overspray-particle-laden air and an outlet opening for the cleaned air, wherein at least one separating electrode (25; 125), which has a separating surface, and a counter electrode device (26; 126) are arranged in the housing (19);c) a high voltage source, whereof the poles can be connected to the separating electrode (25; 125) and the counter electrode device (26);d) an air path for the overspray-particle-laden air, which leads from the base of the coating booth (2) to the inlet opening (15) of the separating device (14);whereine) each separating electrode (25; 125) is associated with a supply device (80; 180) that enables separating fluid to be supplied to the upper region of each separating surface of the separating electrode (25; 125) in such a way that the separating fluid flows extensively over each separating surface of the separating electrode (25; 125);characterized in thatf) the supply device (80; 180) has a supply channel (81; 181) which can be filled to a certain level with separating fluid and is formed in its lower region by two spring steel plates (84, 85; 184; 185) which resiliently lie at least sometimes and at least partially with their respective lower edges against opposite operating surfaces of the separating electrode (25; 125);g) two sliding plates (99, 100; 199, 200) are provided, which lie displaceably against opposite separating surfaces of the separating electrode (25; 125);h) an actuating device (103; 203) is provided, by means of which the sliding plates (99, 100; 199, 200) can be moved back and forth between a position in which their lower edges are located above the lower edges of the spring steel plates (84, 85; 184; 185) and a position in which their lower edges are located below the lower edges of the spring steel plates (84, 85; 184; 185).
- A system (1) according to claim 1, characterized in that the lower edges of the spring steel plates (184; 185) have a crenellated shape or resemble a blunt comb.
- A system (1) according to claim 1 or 2, characterized in that a device (91, 94, 94; 210) is provided, by means of which the lower edges of the spring steel plates (84, 85; 184; 185) can be moved away from the system at the separating surfaces of the separating electrode (25; 125) to an extent that the contents of the supply channel (81; 181) can run out.
- A system (1) according to one of the preceding claims, characterized in that it is designed for painting objects.
- A system (1) according to one of the preceding claims, characterized in that the objects are vehicle bodies.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE102010007479A DE102010007479B3 (en) | 2010-02-09 | 2010-02-09 | Equipment for coating objects |
PCT/EP2011/000414 WO2011098222A1 (en) | 2010-02-09 | 2011-01-29 | System for coating, in particular painting, objects, in particular vehicle bodies |
Publications (2)
Publication Number | Publication Date |
---|---|
EP2533907A1 EP2533907A1 (en) | 2012-12-19 |
EP2533907B1 true EP2533907B1 (en) | 2015-09-16 |
Family
ID=43733275
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP11703385.2A Not-in-force EP2533907B1 (en) | 2010-02-09 | 2011-01-29 | System for coating, in particular painting, objects, in particular vehicle bodies |
Country Status (6)
Country | Link |
---|---|
US (1) | US9126221B2 (en) |
EP (1) | EP2533907B1 (en) |
JP (1) | JP5833573B2 (en) |
CN (1) | CN102753273B (en) |
DE (1) | DE102010007479B3 (en) |
WO (1) | WO2011098222A1 (en) |
Families Citing this family (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE102012009723A1 (en) * | 2012-05-16 | 2013-11-21 | Eisenmann Ag | Device for separating overspray and installation with such |
DE102012023554A1 (en) | 2012-12-01 | 2014-06-05 | Eisenmann Ag | Separator unit for use in an overspray separator |
WO2015082522A1 (en) * | 2013-12-04 | 2015-06-11 | Thomas Mayer | Compressed air treatment chamber |
DE102014018903A1 (en) * | 2014-12-17 | 2016-06-23 | Eisenmann Se | Apparatus and method for separating particles from an exhaust air stream of a coating booth |
KR102221735B1 (en) * | 2019-05-31 | 2021-03-03 | 주식회사 리트코 | Variable bidirectional voltage electrostatic filter system in which the distance between the charging part and the dust collecting part is controlled |
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US1959752A (en) * | 1932-03-09 | 1934-05-22 | Research Corp | Liquid flushing for discharge electrodes |
US3000641A (en) * | 1960-02-24 | 1961-09-19 | Arthur L Walborn | Spreader for attachment to vehicle bodies |
US3724416A (en) * | 1970-05-28 | 1973-04-03 | Allis Chalmers Mfg Co | Electrostatic resin powder spray system having improved powder dispensing means |
JPS6026585B2 (en) * | 1976-10-29 | 1985-06-24 | 三機工業株式会社 | Electric dust collector dust collector plate cleaning device |
JPS5742521Y2 (en) * | 1979-07-19 | 1982-09-18 | ||
US4898116A (en) * | 1987-09-14 | 1990-02-06 | Onoda Cement Company, Ltd. | Powder coating booth |
SE463604B (en) * | 1989-04-25 | 1990-12-17 | Flaekt Ab | DEVICE FOR PURIFICATION OF PREPARED PARTICLES POLLUTANTS VENTILATION AIR FROM A SPRAY BOX BEFORE PAINTING |
EP0415486B1 (en) * | 1989-08-31 | 1994-03-16 | METALLGESELLSCHAFT Aktiengesellschaft | Process and apparatus for electrostatic cleaning of noxious and dusty exhaust gases in multiple field separators |
DE4018488C1 (en) * | 1990-06-09 | 1991-10-02 | Metallgesellschaft Ag, 6000 Frankfurt, De | Removing dust and hazardous materials from waste gases - by sepg. dust in dry multi-cyclone stage, and wet electrostatic precipitator stage |
US5160510A (en) | 1990-06-09 | 1992-11-03 | Metallgesellschaft Aktiengesellschaft | Process and apparatus for purifying dust- and pollutant-containing exhaust gases |
JPH04141266A (en) * | 1990-09-29 | 1992-05-14 | Taikisha Ltd | Coating facility |
DE19720005C1 (en) * | 1997-05-13 | 1998-11-19 | Wagner Int | Device for separating excess powder, which is obtained during the powder coating of workpieces |
JP2000354787A (en) * | 1999-04-15 | 2000-12-26 | Watanabe Seisakusho:Kk | Wet electric dust collector |
DE10231503A1 (en) * | 2002-07-12 | 2004-02-12 | EISENMANN Maschinenbau KG (Komplementär: Eisenmann-Stiftung) | Process for coating, in particular painting objects |
DE102004001095A1 (en) * | 2004-01-05 | 2005-07-28 | Blue Membranes Gmbh | RF sputtering |
DE102005013711B4 (en) * | 2005-03-24 | 2022-07-28 | Dürr Systems Ag | Plant for painting objects |
JP2008212846A (en) * | 2007-03-05 | 2008-09-18 | Hitachi Plant Technologies Ltd | Water flow mechanism of wet electrostatic dust precipitator |
EP2011575A1 (en) * | 2007-07-05 | 2009-01-07 | Envirtek A/S | A collecting electrode for a liquid flushed electrical precipitator |
DE102007036553A1 (en) * | 2007-07-25 | 2009-02-05 | Eisenmann Anlagenbau Gmbh & Co. Kg | Device for separating paint overspray |
DE102008046414A1 (en) * | 2008-09-04 | 2010-03-18 | Eisenmann Anlagenbau Gmbh & Co. Kg | Device for separating paint overspray |
DE102009058206A1 (en) * | 2009-12-15 | 2011-06-16 | Eisenmann Anlagenbau Gmbh & Co. Kg | Method and device for separating overspray and installation with such |
-
2010
- 2010-02-09 DE DE102010007479A patent/DE102010007479B3/en not_active Expired - Fee Related
-
2011
- 2011-01-29 WO PCT/EP2011/000414 patent/WO2011098222A1/en active Application Filing
- 2011-01-29 JP JP2012552292A patent/JP5833573B2/en not_active Expired - Fee Related
- 2011-01-29 EP EP11703385.2A patent/EP2533907B1/en not_active Not-in-force
- 2011-01-29 CN CN201180008686.3A patent/CN102753273B/en not_active Expired - Fee Related
- 2011-01-29 US US13/577,299 patent/US9126221B2/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
EP2533907A1 (en) | 2012-12-19 |
CN102753273A (en) | 2012-10-24 |
WO2011098222A1 (en) | 2011-08-18 |
JP2013518719A (en) | 2013-05-23 |
JP5833573B2 (en) | 2015-12-16 |
US20120304925A1 (en) | 2012-12-06 |
CN102753273B (en) | 2015-04-29 |
US9126221B2 (en) | 2015-09-08 |
DE102010007479B3 (en) | 2011-06-22 |
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